CN101338051B - Long glass fiber reinforced polypropylene material and preparation thereof - Google Patents
Long glass fiber reinforced polypropylene material and preparation thereof Download PDFInfo
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- CN101338051B CN101338051B CN2008100209365A CN200810020936A CN101338051B CN 101338051 B CN101338051 B CN 101338051B CN 2008100209365 A CN2008100209365 A CN 2008100209365A CN 200810020936 A CN200810020936 A CN 200810020936A CN 101338051 B CN101338051 B CN 101338051B
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- 239000004743 Polypropylene Substances 0.000 title claims abstract description 86
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- -1 polypropylene Polymers 0.000 title claims abstract description 75
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- RKISUIUJZGSLEV-UHFFFAOYSA-N n-[2-(octadecanoylamino)ethyl]octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NCCNC(=O)CCCCCCCCCCCCCCCCC RKISUIUJZGSLEV-UHFFFAOYSA-N 0.000 claims description 5
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- BGYHLZZASRKEJE-UHFFFAOYSA-N [3-[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxy]-2,2-bis[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxymethyl]propyl] 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)OCC(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 BGYHLZZASRKEJE-UHFFFAOYSA-N 0.000 claims description 4
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Abstract
The invention provides a long glass fiber reinforced polypropylene material and a preparation method thereof. The mass ratio of the material components is: 35 percent to 55 percent of polypropylene, 35 percent to 50 percent of long glass fibers, 0.3 percent to 0.8 percent of coupling agents, 5 percent to 10 percent of compatilizers, 2 percent 4 percent of flow modifiers, 0.3 percent to 0.6 percent of antioxidants and 1 percent to 2 percent of lubricants. The invention has the process that the polypropylene, the flow modifiers, the compatilizers, the antioxidants and the lubricants are mixed firstly, then the mixture is added into a double screw extruder, and the processing temperature is 180 DEG C to 230 DEG C; a molten bath is formed by extruding melts from the extruding die of the extruder; the continuous long glass fibers are preheated for drying, and the surfaces of the long glass fibers are processed; later, a soakage device is introduced to lead a plurality of strands of the long glass fibers into the molten bath so that the long glass fibers are completely soaked and then is bundled to be packaged, and finally, the long glass fibers are discharged from a bell-mouthed die head outlet to be cooled and cut into granules to obtain the long glass fiber reinforced polypropylene granule materials. The invention has simple and practical process and favorable product performance.
Description
Technical field
The present invention relates to glass filament reinforced plastics, relate in particular to a kind of long glass fiber reinforced polypropylene material and preparation method thereof, belong to technical field of polymer materials.
Background technology
Glass filament reinforced plastics is a kind of light-high-strength structural timber.Its stretching, bending elastic modulus and creep resistance, resistent fatigue characteristic are much better than non-reinforced plastics, and major cause is, do the time spent as external force, and load is by the fiber transmission, and fiber has good mechanical property.In West Europe, there are 50% fibre reinforced plastics to be applied to automotive industry approximately, in the U.S. about 30%.Roving glass fiber reinforced thermoplastics(RTP) (LFRT) has superior stiffness, toughness, anti-warpage properties and UV stable, and price is lower than ABS and engineering plastics.Because mean fibre length is longer in the goods, and macrofiber can form certain network structure in injection-molded item, so the mechanical property of goods all is better than chopped strand reinforced plastics with other physicalies.LFRT is widely used in automobile, field of household appliances, and annual growth is 20～30%.Wherein that the output maximum is long fibre enhanced polypropylene alkene (LGFPP).
Long glass fibres reinforced plastics performance depends primarily on following factor: 1. glass fiber content, and in general, glass fiber content is high more, the mechanical property of glass reinforced plastics is also high more, but glass fiber content is too high, to the processing units serious wear, and material fragility is improved and the density increase; 2. the length of glass in resin matrix; 3. the good cohesive force of glass and resin matrix is uniformly dispersed.
LGFPP produces at present, the dipping effect of most its glasses of product in polypropylene matrix is not ideal enough, and also there is certain defective in dispersion and the orientation of glass in polypropylene, causes the performance of product not ideal enough, the mechanical property improvement of still needing, but also can have the glass emergence on the surface phenomenon.
Summary of the invention
The objective of the invention is to overcome the deficiency that prior art exists, a kind of long glass fiber reinforced polypropylene material and preparation method thereof is provided, utilization scientific formula and fiberglass surfacing treatment technology, be intended to strengthen the dipping effect of glass in melt, eliminate the phenomenon that exposes of glass, improve the smooth finish of material, effectively improve the mechanical property of material.
Purpose of the present invention is achieved through the following technical solutions:
Long glass fiber reinforced polypropylene material, characteristics are that the quality percentage composition of component is: polypropylene 35～55wt%, long glass fibres 35～50wt%, coupling agent 0.3～0.8wt%, compatilizer 5～10wt%, flow ability modifying agent 2～4wt%, oxidation inhibitor 0.3～0.6wt%, lubricant 1～2wt%.
Further, above-mentioned long glass fiber reinforced polypropylene material, its component ideal mass percent is: polypropylene 38wt%, long glass fibres 50wt%, coupling agent 0.5wt%, compatilizer 6wt%, flow ability modifying agent 4wt%, oxidation inhibitor 0.5wt%, lubricant 1wt%.
Further, above-mentioned long glass fiber reinforced polypropylene material is characterized in that: described polypropylene be in the molten polypropylene that refers to, in molten refer to polypropylene be in the molten homo-polypropylene that refers to, co-polypropylene a kind of or their mixture; Melting index is at 10～25g/10min.Described long glass fibres is the continuous roving of LFRT, and fiber type is an E glass, and Fibre diameter is 17um.Described coupling agent is one or more the mixture in coupling agent KH-550, coupling agent KH-560, the complex ester class coupling agent.Described compatilizer is the maleic anhydride inoculated polypropylene compatilizer.Described flow ability modifying agent is the PP cooling masterbatch.Described oxidation inhibitor is one or more the mixture among antioxidant 1010, oxidation inhibitor 1790, oxidation inhibitor 1098, oxidation inhibitor 168, the oxidation inhibitor DLTDP.Described lubricant is a kind of in ethylene bis stearamide, high molecular (molecular weight 7000～9000) Poly Propylene Wax or their mixture.
Further, the preparation method of long glass fiber reinforced polypropylene material may further comprise the steps
(a) polypropylene, flow ability modifying agent, compatilizer, oxidation inhibitor and lubricant are joined to make it thorough mixing in the mixing machine even;
(b) the above-mentioned mixture that obtains is joined in the twin screw extruder by charging opening, processing temperature is at 180～230 ℃, and totally six sections of twin screw extruders, first section and second section extrusion temperature are at 180～200 ℃, and other several sections extrusion temperatures are at 200～230 ℃; The residence time of material in twin screw extruder is 3～8min, and engine speed is controlled at 250～350r.min
-1Then, by twin screw extruder mouth mould melt extrusion, and be transported to and form the molten bath in the immersion system;
(c), make its surface temperature reach 60～80 ℃ with the continuous long glass fiber preheating and drying; Then make the liquid coupling agent of long glass fibres surface infiltration, and impel each section chief's glass fibre clocklike to disperse and boundling by the roving glass fiber surface processing device; Introduce immersion system subsequently, several section chief's glass fibre are introduced in the molten bath of immersion system, under melt pressure and tension force effect, long glass fibres is fully flooded by melt by pressure roller, enter the boundling coating unit again and carry out the boundling coating, then from the die head exit discharging of toroidal, cooling, pelletizing promptly obtain the long glass fiber reinforced polypropylene pellet at last.
Substantive distinguishing features and obvious improvement that technical solution of the present invention is outstanding are mainly reflected in:
The present invention has adopted the optimization design and the comprehensive synergistic effect of coupling agent, compatilizer, flow ability modifying agent and lubricant, with specific component, specific percentage of grafting and the graft modification polypropylene of melt index is compatilizer, improves the interface binding power of polypropylene and roving glass fiber greatly; With the controllable rheology polypropylene cooling masterbatch is flow ability modifying agent, reduces melt viscosity; The adding of coupling agent, lubricant can improve the dispersiveness of glass in matrix.By surface treatment and melt impregnation technology to glass fibre, improve the mechanical property of long glass fiber-reinforced polypropylene, efficiently solve the problem that exposes of glass, improve the smooth finish of matrix material.The long glass fiber reinforced polypropylene of being produced can satisfy the service requirements of high-strength vehicle accessory, and alternative enhancement engineering plastics are used to produce automobile, household electrical appliances parts etc.And preparation process is simple, and production technique is controlled easily, and productive rate is higher, has reduced raw materials cost, and the economic benefit highly significant is worthy of popularization.
Description of drawings
Below in conjunction with accompanying drawing technical solution of the present invention is described further:
Fig. 1: the structural representation that is used to produce the equipment of long glass fiber reinforced polypropylene material.
The implication of each Reference numeral sees the following form among the figure:
| Reference numeral | Implication | Reference numeral | Implication | Reference numeral | Implication |
| 1 | Long glass fibres | 2 | The roving glass fiber primary heater unit | 3 | The roving glass fiber surface processing device |
| 4 | Liquid coupling agent transferpump | 5 | The reducing pressure roller | 6 | Liquid coupling agent atomisation unit |
| 7 | Liquid recovery tube | 8 | Preceding guide roller | 9 | The forcing machine junctor |
| 10 | The melt distribution device | 11 | Middle guide roller | 12 | Pressure roller |
| 13 | Pressure roller | 14 | Back guide roller | 15 | The boundling coating unit |
| 16 | Flaring exit | 17 | Refrigerating unit | 18 | Take off roll |
| 19 | Take off roll | 20 | Pellet device | 21 | Twin screw extruder |
Embodiment
The present invention develops a kind of long glass fiber reinforced polypropylene material, by surface treatment and melt impregnation technology to the selection of relevant auxiliary agents such as long glass fibres, compatilizer, proportioning, glass fibre, improve the mechanical property of long glass fiber-reinforced polypropylene (LGFPP), effectively solve the problem that exposes of glass simultaneously, improve the smooth finish of matrix material.
Long glass fiber reinforced polypropylene material, the mass ratio of its component is: polypropylene 35～55wt%, long glass fibres 35～50wt%, coupling agent 0.3～0.8wt%, compatilizer 5～10wt%, flow ability modifying agent 2～4wt%, oxidation inhibitor 0.3～0.6wt%, lubricant 1～2wt%.The ideal proportioning is: polypropylene 38wt%, long glass fibres 50wt%, coupling agent 0.5wt%, compatilizer 6wt%, flow ability modifying agent 4wt%, oxidation inhibitor 0.5wt%, lubricant 1wt%.
Wherein, polypropylene be in the molten polypropylene that refers to, in molten refer to polypropylene be in the molten homo-polypropylene that refers to, co-polypropylene a kind of or their mixture; Melting index is at 10～25g/10min.Long glass fibres is the continuous roving of LFRT, and fiber type is an E glass, and Fibre diameter is 17um.Coupling agent is one or more the mixture in coupling agent KH-550, coupling agent KH-560, the complex ester class coupling agent.Compatilizer is the maleic anhydride inoculated polypropylene compatilizer.Described flow ability modifying agent is the PP cooling masterbatch; Oxidation inhibitor is one or more the mixture among antioxidant 1010, oxidation inhibitor 1790, oxidation inhibitor 1098, oxidation inhibitor 168, the oxidation inhibitor DLTDP.Lubricant is a kind of in ethylene bis stearamide, the high molecular weight polypropylene wax (molecular weight 7000～9000) or their mixture.
Adopt flow production line as shown in Figure 1 to prepare long glass fiber reinforced polypropylene material, this suite of equipment mainly comprises roving glass fiber primary heater unit 2, roving glass fiber surface processing device 3, immersion system, boundling coating unit 15 and twin screw extruder 21 and refrigerating unit 17, towing mechanism, pellet device 20, roving glass fiber primary heater unit 2 and roving glass fiber surface processing device 3 transition and linkages, roving glass fiber surface processing device 3 and immersion system transition and linkage, immersion system and boundling coating unit 15 transition and linkages.Wherein, roving glass fiber primary heater unit 2 is the closed enclosure body structure, and Heating element is installed in the case, and the inwall of casing is provided with thermal insulation layer, the temperature inside the box homogeneous and controllable.Roving glass fiber surface processing device 3 comprises reducing pressure roller 5, liquid coupling agent atomisation unit 6, liquid coupling agent transferpump 4 and the liquid recovery tube 7 of one group of likeness in form spindle, reducing pressure roller 5 disperses and boundling the roving glass fiber of carrying along the reducing roller surface by rational combination, liquid coupling agent atomisation unit 6 is positioned at the below of reducing pressure roller 5 and is right against reducing pressure roller 5, liquid coupling agent transferpump 4 is to liquid coupling agent atomisation unit 6 feed, and the material after 7 pairs of atomizings of liquid recovery tube reclaims.Immersion system is case structure, be provided with forcing machine junctor 9 in it, melt distribution device 10, preceding guide roller 8, middle guide roller 11, back guide roller 14 and a pair of pressure roller (12,13), forcing machine junctor 9 is connected with twin screw extruder 21, twin screw extruder 21 constitutes the melt transfer passage by forcing machine junctor 9 and melt distribution device 10, reducing pressure roller 5 and the transition mutually of preceding guide roller 8, preceding guide roller 8, middle guide roller 11, pressure roller 12, pressure roller 13, back guide roller 14 is transition and linkage successively, pressure roller 12 is stagger arrangement up and down with pressure roller 13 and arranges, boundling coating unit 15 has flaring exit 16, the exit end of boundling coating unit 15 is distributed with refrigerating unit 17 successively, towing mechanism (take off roll 18,19) and pellet device 20, constitute processing line.
Multiple arrangement is by front and back program, horizontally disposed formation continuous processing line, and roving glass fiber primary heater unit 2, roving glass fiber surface processing device 3, immersion system and boundling coating unit 15 are the casing that structure relative closure, profile are rectangular parallelepiped.Long glass fibres 1 is the roving glass fiber primary heater unit 2 by being made up of one group of Heating element at first, and roving glass fiber primary heater unit 2 makes long glass fibres 1 preheating reach certain temperature, so that the long glass fibres drying of one-tenth thigh, loose.Long glass fibres 1 after the preheating enters roving glass fiber surface processing device 3 subsequently, roving glass fiber surface processing device 3 is made of the reducing pressure roller 5 of liquid coupling agent atomisation unit 6 and one group of likeness in form spindle, the liquid coupling agent of preparation fully soaks into the long glass fibres surface by atomisation unit 6, thereby liquid coupling agent obtains good treatment effect with surperficial fully contact of roving glass fiber; The effect of reducing pressure roller 5 is, impels trailed each section chief's glass to be and clocklike to disperse and boundling when fusiform one group of reducing roller surface forward is carried being affixed to the cross section, strengthens roving glass fiber surface-treated effect.The roving glass fiber of handling is pulled and enters the melt impregnation device, the melt impregnation device is connected with twin screw extruder 21 by forcing machine junctor 9, in the twin screw extruder 21 the plastifying polymer melt enter the molten bath that immersion system forms certain altitude via forcing machine junctor 9 and melt distribution device 10, for the roving glass fiber dipping; Trailed roving glass fiber enters the molten bath via preceding guide roller 8 and 11 guiding of middle guide roller, and forwards carries along pressure roller 12, pressure roller 13 surfaces; Pressure roller 12 can be regulated according to particular case with the upper-lower position of pressure roller 13 with the spacing and the pressure roller 12 of pressure roller 13; It is relevant that fiber impregnation effect and pressure roller and fiber press power indirectly, the roving glass fiber of dipping is finished boundling and coating via boundling coating unit 15 and flaring exit 16, the desired quality of runner direction controllable size system product of control boundling coating unit 15 and flaring exit 16 makes long glass fibres reach the good melt impregnation and the effect of melt coating.
During concrete the preparation, as described below.
Embodiment 1:
With the molten homo-polypropylene that refers in 54.4 parts, 5 parts of maleic anhydride inoculated polypropylene compatilizers, 4 parts of PP cooling masterbatchs, 0.1 part of oxidation inhibitor 1790 and 0.2 part of oxidation inhibitor DLTDP, 1 part of ethylene bis stearamide join that to make it thorough mixing in the mixing machine even.Mixture is added in the twin screw extruder by charging opening, and processing temperature is at 185～230 ℃, and the control of twin screw extruder temperature is provided with six sections, and first section and second section extrusion temperature are at 185～200 ℃, and other several sections extrusion temperatures are at 210～230 ℃; The residence time of material in twin screw extruder is 8min, and engine speed is 300～350r.min
-1Then form the molten bath by twin screw extruder mouth mould melt extrusion.With 35 parts of continuous long glass fiber preheating and dryings, make its surface temperature reach 65～80 ℃, then the long glass fibres surface is handled by the glass surface processing device, make 0.3 part of coupling agent KH-550 of long glass fibres surface infiltration; Then introduce the dipping head, several section chief's glass fibre are introduced in the molten bath, under melt pressure and tension force effect, long glass fibres is fully flooded by pressure roller, entering beaming device again coats, then from the head exit discharging of toroidal, cooling, pelletizing promptly obtain the long glass fiber reinforced polypropylene pellet at last.
Embodiment 2:
With the molten co-polypropylene that refers in 43.6 parts, 10 parts of maleic anhydride inoculated polypropylene compatilizers, 3 parts of PP cooling masterbatchs, 0.2 part of oxidation inhibitor 1098 and 168,2 parts of high molecular weight polypropylene waxes of 0.4 part of oxidation inhibitor join that to make it thorough mixing in the mixing machine even.Mixture is added in the twin screw extruder by charging opening, and processing temperature is at 180～230 ℃, and the control of twin screw extruder temperature is established six sections altogether, and first section and second section extrusion temperature are at 180～200 ℃, and other several sections extrusion temperatures are at 200～230 ℃; The residence time of material in twin screw extruder is 3min, and engine speed is 250～350r.min
-1Then form the molten bath by twin screw extruder mouth mould melt extrusion.With 40 parts of continuous long glass fiber preheating and dryings, make its surface temperature reach 60～75 ℃; Then the long glass fibres surface is handled, make 0.8 part of coupling agent KH-560 of long glass fibres surface infiltration by the glass surface processing device; Introduce the dipping head subsequently, several section chief's glass fibre are introduced in the molten bath, under melt pressure and tension force effect, long glass fibres is fully flooded by pressure roller, entering beaming device again coats, then from the head exit discharging of toroidal, cooling, pelletizing promptly obtain the long glass fiber reinforced polypropylene pellet at last.
Embodiment 3:
Refer to the molten homo-polypropylene that refers in the co-polypropylene, 23 parts with molten in 15 parts, 6 parts of maleic anhydride inoculated polypropylene compatilizers, 4 parts of PP cooling masterbatchs, 0.2 part antioxidant 1010 and 168,0.5 parts of high molecular weight polypropylene waxes of 0.3 part of oxidation inhibitor, 0.5 part of ethylene bis stearamide join, and to make it thorough mixing in the mixing machine even.Mixture is added in the twin screw extruder by charging opening, and processing temperature is at 190～230 ℃, and the control of twin screw extruder temperature is provided with six sections, and first section and second section extrusion temperature are at 190～200 ℃, and other several sections extrusion temperatures are at 200～230 ℃; The residence time of material in twin screw extruder is 5min, and engine speed is 250～300r.min
-1Then form the molten bath by twin screw extruder mouth mould melt extrusion.With 50 parts of continuous long glass fiber preheating and dryings, make its surface temperature reach 60～80 ℃, then the long glass fibres surface is handled, make 0.5 part of coupling agent of long glass fibres surface infiltration (coupling agent KH550 mixes with complex ester class coupling agent) by the glass surface processing device; Introduce the dipping head subsequently, several section chief's glass fibre are introduced in the molten bath, under melt pressure and tension force effect, long glass fibres is fully flooded by pressure roller, entering beaming device again coats, then from the head exit discharging of toroidal, cooling, pelletizing promptly obtain the long glass fiber reinforced polypropylene pellet at last.
After testing, the long glass fiber-reinforced polypropylene materials that adopts the technical solution of the present invention preparation is compared with Korea S import same type of material, and its Main physical performance index see Table 1.
Table 1
| Test item | Embodiment 1 | Embodiment 2 | Embodiment 3 | Comparative example |
| Tensile strength (MPa) | 124 | 132 | 143 | 101.2 |
| Elongation at break (%) | 12 | 11 | 11.5 | 10.5 |
| Flexural strength (MPa) | 155 | 176 | 184 | 140 |
| Modulus in flexure (MPa) | 6420 | 7650 | 9230 | 4945 |
| Simply supported beam notched Izod impact strength (KJ/m 2) | 21 | 30.5 | 34 | 14.6 |
| Heat-drawn wire (℃) | 158 | 163 | 171 | 152.3 |
| Rockwell hardness | 110 | 111 | 113 | 110 |
The present invention is a compatilizer with specific component, specific percentage of grafting and the graft modification polypropylene of melt index, improves the interface binding power of polypropylene and roving glass fiber greatly; With the controllable rheology polypropylene cooling masterbatch is flow ability modifying agent, reduces melt viscosity; With the lubricant is dispersion agent, improves the dispersiveness of glass in matrix.By surface treatment and melt impregnation technology to glass fibre, improve the mechanical property of long glass fiber-reinforced polypropylene, efficiently solve the problem that exposes of glass, improve the smooth finish of matrix material.The long glass fiber reinforced polypropylene of being produced has good technical performance, can satisfy the service requirements of high-strength vehicle accessory, and alternative enhancement engineering plastics are used to produce automobile, household electrical appliances parts etc.And preparation process is simple, and production technique is controlled easily, and productive rate is higher, greatly reduces raw materials cost, has brought very significantly economic benefit, and application prospect is very good.
Below only be concrete exemplary applications of the present invention, protection scope of the present invention is not constituted any limitation.All employing equivalents or equivalence are replaced and the technical scheme of formation, all drop within the rights protection scope of the present invention.
Claims (10)
1. long glass fiber reinforced polypropylene material, the quality percentage composition that it is characterized in that its component is: polypropylene 35～55wt%, long glass fibres 35～50wt%, coupling agent 0.3～0.8wt%, compatilizer 5～10wt%, flow ability modifying agent 2～4wt%, oxidation inhibitor 0.3～0.6wt%, lubricant 1～2wt%.
2. long glass fiber reinforced polypropylene material according to claim 1, it is characterized in that its component has following mass percent: polypropylene 38wt%, long glass fibres 50wt%, coupling agent 0.5wt%, compatilizer 6wt%, flow ability modifying agent 4wt%, oxidation inhibitor 0.5wt%, lubricant 1wt%.
3. long glass fiber reinforced polypropylene material according to claim 1 and 2 is characterized in that: described polypropylene be in the molten polypropylene that refers to, in molten refer to polypropylene be in the molten homo-polypropylene that refers to, co-polypropylene a kind of or their mixture; Melting index is at 10～25g/10min.
4. long glass fiber reinforced polypropylene material according to claim 1 and 2 is characterized in that: described long glass fibres is the continuous roving of LFRT, and fiber type is an E glass, and Fibre diameter is 17 μ m.
5. long glass fiber reinforced polypropylene material according to claim 1 and 2 is characterized in that: described coupling agent is one or more the mixture in coupling agent KH-550, coupling agent KH-560, the complex ester class coupling agent.
6. long glass fiber reinforced polypropylene material according to claim 1 and 2 is characterized in that: described compatilizer is the maleic anhydride inoculated polypropylene compatilizer.
7. long glass fiber reinforced polypropylene material according to claim 1 and 2 is characterized in that: described flow ability modifying agent is the PP cooling masterbatch.
8. long glass fiber reinforced polypropylene material according to claim 1 and 2 is characterized in that: described oxidation inhibitor is one or more the mixture among antioxidant 1010, oxidation inhibitor 1790, oxidation inhibitor 1098, oxidation inhibitor 168, the oxidation inhibitor DLTDP.
9. long glass fiber reinforced polypropylene material according to claim 1 and 2, it is characterized in that: described lubricant is a kind of in ethylene bis stearamide, the high molecular weight polypropylene wax or their mixture, wherein, the molecular weight of high molecular weight polypropylene wax is 7000～9000.
10. the preparation method of the described long glass fiber reinforced polypropylene material of claim 1 is characterized in that: may further comprise the steps---
(a) polypropylene, flow ability modifying agent, compatilizer, oxidation inhibitor and lubricant are joined to make it thorough mixing in the mixing machine even;
(b) the above-mentioned mixture that obtains is joined in the twin screw extruder by charging opening, twin screw extruder temperature control is established six sections altogether, and first section and second section extrusion temperature are at 180～200 ℃, and other several sections extrusion temperatures are at 200～230 ℃; The residence time of material in twin screw extruder is 3～8min, and engine speed is controlled at 250～350r.min
-1Then, by twin screw extruder mouth mould melt extrusion, and be transported to and form the molten bath in the immersion system;
(c), make its surface temperature reach 60～80 ℃ with the continuous long glass fiber preheating and drying; Then make the liquid coupling agent of long glass fibres surface infiltration, and impel each section chief's glass fibre clocklike to disperse and boundling by the roving glass fiber surface processing device; Introduce immersion system subsequently, several section chief's glass fibre are introduced in the molten bath of immersion system, under melt pressure and tension force effect, long glass fibres is fully flooded by melt by pressure roller, enter the boundling coating unit again and carry out the boundling coating, then from the die head exit discharging of toroidal, cooling, pelletizing promptly obtain the long glass fiber reinforced polypropylene pellet at last.
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2008
- 2008-08-08 CN CN2008100209365A patent/CN101338051B/en not_active Expired - Fee Related
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| CN102382370A (en) * | 2011-10-18 | 2012-03-21 | 深圳市科聚新材料有限公司 | Polypropylene engineering plastic as well as preparation method and application thereof |
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